Stabilization of polyesters from dihydric alcohols and both saturated and unsaturated dicarboxylic acids



condensates. I I larly in vacuo or in a current of an inert gas, A condensation continues linearly with formation NITE "-srATEs PATENT OFFICE v 2.43723ZI I sranmrzanon orfronmsrsns FROM m- I nrmuc ALconoLs AND BOTH SATURAT- ACIDS ED AND UNSATUR ATED DICARBOXYLIO David A. Bothrock, 1.. one mohora r. Oonyne, Pa assign'ors, to The Reslnous rroooouaohemioei Company, a corporation 'No Drawing. application October is,

I 194:, Serial No. 506,432. .Dlvided and um applioatlon November 21, 1945, Serial No. 630,128

invention relates Serial N .5oa432, filed October 15, 1943, I

, 'It has long been known that when a dihydric or a. simple ester of a dibasic acid and a volatile monohydric alcohol, are heated together polymeric esters result. Thesepolyesters are linear As heating is continued, particuo! longer'and longer chains. The products thus obtained vary rifrom gummy products through waxy to hard or crystalline products, depending uponchoice. ofreactants and conditions of reaction; At high molecular weights, some of the linearcondensation polymers are capable of being 'oold-diawntinto fibers. But not all applications'ol these polyesters arexdependent upon this property. The polyesters are useful for. a great varietyoi' other purposes,- such as coatin adhering, extruding, molding, casting, laminating, or modifying other resinous or polymeric materials, including synthetic rubbers. The intended use'generally determines the choice of dibasic acid and of dihydric alcohol and the extent to which the condensation polymerization oi. the polyester is carried. For many purposes polymers having molecular weights of at least five'thousand are desired and, in many applicai Claims. (Cl. 260-75) I to new compositions of matter and to the procesgby which they are formed. :.More particularly, it relates to improvementsin. condensation polymers and to improvementsintheir-stability.

" This application isv a division of application may tend to become more viscous.

tions, polyesters having molecular weights of eight thousand, or twelve thousand, or even more are particularly valuable. In general, with high molecular weight it becomes more difllcult to maintain theproperties which are dependent upon such molecular weight.

In applying polyesters, there are many advantages in using them in the molten form. In

air and/or moisture, however, the molten polyesters degrade as heating is continued. The

' changes appear to be due to both oxidation and hydrolysis, but, according to at least one theory of this degradation, oxidation of reactive groups supplies water for. splitting the ester linkages. to

Similar degradation of the polyesters occurs on agin particularly in light. Whatever the mechanism of degradation, the degraded polyesters are less useful than the original polyesters, and the degraded material often fails for its intended p p ses.

On the other hand, some polyesters are unstable in another way. It the hot melted products are maintained under an inert atmosphere to avoid degradation during application, they This may so alter the properties as to interfere with the proper extruding, coating, or appiying of the polyester. While acylation of the terminal hydroxyl groups of a linear polyester may be used to inhibit an increase in viscosity of melted polymer, this reaction does not assure stabilization in other respects.

The prima y. objects of this invention are to provide a method for stabilizing polyesters of high molecular weight and to provide polyesters stabilized against changes due to continued polymerization or to degradation. It is also an object to provide new polymeric compositions which are capable 01' being extruded, coated, molded, or otherwise shaped or applied from "hot melts" and which retain the desired degree of viscosity, plasticity, toughness, and other properties during and after the application thereof. It is thus an object to stabilize polyesters based on dibasic acids and dihydric a1- cohols, particularly those of high molecular weight. It is a particular object to lessen markedly the degradation from air, light, and moisture of highly polymerized esters derived from such acids and alcohols.

We have found that these objects are accomplished by preparing a polymeric condensate of a dibasic carboxylic'acid and a dihydric alcohol, carrying the linear condensation thereof to an intermediate stage or approximately to the degree of condensation most suitable for the intended application, adding thereto at this stage an ester-forming compound having a functionality greater than two, and heating the resulting mixture until the said polymeric condensate and the said ester-forming compound have reacted. 'I'hefinal heating is preferably performed under an inert gasand/or underlreduced pressure.

The mere admixture of a polyfunctional, stabilizing ester-forming agent to the linear condensation polyester fails to accomplish the objects of this invention. On the other hand, the optimum effects are not obtained from the polyfunctional, stabilizing ester-forming agent when it is mixed with a dihydric alcohol and a dibasic ester-forming carboxylic compound andall of these componentsthen reacted. In generaLthe polymeric products thus obtained lack the properties and advantages inherent in the polymers prepared according to this invention.

For the preparation of the linear polyester, there maybe used as dlhydric alcohols any of the alkylene or polyalkylene glycols, including ethylene glycol, trimethylene glycol, propylene glycol, the various butylene glycols, hexylene glycol, octylene glycol, dodecylene glycol, diethylene glycol, triethylene glycol, tetraethylene glycol, or the like, cyclohexanediols, 1,2-di-B-hydroxyethyl benzene, di-s-hydroxyethoxy benzene, 2,2- (di-fi-hydroxyethoxyphenyl) propane, xylylene glycols, thiotriethylene glycol, or other dihydric alcohol so long as it is free from groups other than hydroxyl reacting with carboxylic groups. Equivalent to the dihydric alcohols are the halides thereof, which, as is known, may be reacted with salts of dibaslc acids to form linear condensation polymers. There may be used a single dihydric alcohol or a mixture of such alcohols and, like wise, a single dibasic carboxylic acid or a mixture of such acids. The only known limitation as to choice of the two main reactants lies in the fact that when the combined chain length of alcohol plus acid is five or six atoms, cycles tend to form rather than chain polymers.

The preferred class of dihydric alcohols includes those of the formula:

HO (CH2) nOH wherein n is an integer of at least two. These are the alkylene glycols, available with alkylene groups of two to twelve or more carbon atoms. The groups may be straight or branched chained.

As suitable dibasic acids, there may be used one or more of such acids as oxalic, succinlc, glutaric, e-methyl glutaric, a-ethyl glutaric, adipic, s-methyl adipic, pimelic, suberic, azelaic, sebacic, brassilic, tetradecanedioic, paraphenylene diacetic, 2,2-dl-carboxymethoxyphenyl propane, phthalic, terephthalic, hexahydroterephthalic, isophthalic, diglycolic, thiodibutyric, diphenic, or the like dicarboxylic acid. Individual acids or mixtures of acids may be used. Particularly in such mixtures, there may be used unsaturated aliphatic acids such as maleic, fumaric, or dihydromuconic. Instead of the acids themselves, there may be used with suitable change in the esterification process the corresponding anhydrides, where such exist, such as succinlc, maleic, or sebacic anhydrides, or acid halides, such as succinyl chloride or adipyl bromide, salts such as potassium adipate, or esters of a volatile alcohol, such as ethyl pimelate or methyl sebacate. In general, any poly-ester forming derivative of a dibasic acid or the acid itself may be reacted with a. dihydric alcohol or an ester-forming derivative thereof.

The preferred class of dibasic carboxylic acids may be represented by the formula:

HOOC (CI-H) mCOOH wherein m is an integer having a value of at least two. The known acids coming within this formula are the saturated dibasic aliphatic carboxylic acids from succinic acid upwards. These 4, dibasic acids may be used as pure entities or in mixtures of the various dibasic acids of this type. Mixtures of a preferred type of dibasic acid with other types of dibasic acids may also be used. Some of the most useful mixtures are with such acids as phthalic or maleic in which the latter constitute the minor proportion.

The primary reactions between dibasic acid or derivative and dihydric alcohol or derivative are known, and the formation of linear condensation polymers therefrom has already been given considerable study. Usually, when excess of acid is used, the terminal groups of the polymers are primarily carboxylic while, when excess of glycol is used, the terminal groups are primarily hydroxyl. When polymers of rather high molecular weights, let us say above three thousand to five thousand, are desired, it is usually desirable .to start with an excess of the more volatile constituent, which excess may be removed at an advanced stage of polymerization by a method such as heating with distillation of the excess constituent under reduced pressure. When an excess of glycol is used, the terminal groups of the polymeric chains are primarily hydroxyl groups, as has been indicated. In promoting the degree of polymerization or in increasing the molecular weight of the linear condensates, continued heating is generally resorted to, preferably under reduced pressure to assist in the removal of the water, alcohol, hydrogen halide, or the like, when these are formed in the condensation. A volatile product formed may similarly be removed by passage of a gas, particularly one such as hydrogen or nitrogen, which is inert. Condensation by heating is continued until the type of polymer desired is almost reached. The degree of condensation or polymerization at this point will vary considerably, depending on the properties desired in the final condensates and the choice of difunctional reactants and the presence or absence of a catalyst.

As catalysts there have been proposed acidic substances, such as toluene sulfonic acid and zinc chloride. These greatly accelerate the formation of high polymers, but they also lessen the stability of polymers formed therewith.

The condensation may be carried to different degrees of polymerization to attain certain properties. For example, if waxy or crystalline polymer is desired, the degree of polymerization may be lower, other things being equal, than when tough, flexible polymers are desired. If polymers which can be drawn into fibers or films are required, then relatively high molecular weights are preferably attained before stabilization is accomplished.

The condensate brought to approximately the desired degree of polymerization, as shown by a test such as that for intrinsic viscosity or melt viscosity, is treated with a stabilizing agent consisting of an ester-forming compound having an ester-forming functionality greater than two. Trifunctional ester-forming compounds are preferred as stabilizers. Such polyfunctional esterforming compounds include their derivatives which yield these compounds in reaction, inasmuch as they react in the system to produce the same effect. The polyfunctional stabilizing compounds include tricarboxylic acids, tetracarboxylic acids, and higher carboxylic acids, their esters, anhydrides, acyl halides, acid amides, and salts, including their amine salts. The polyfunctional stabilizing compounds also include trillilydsric, tetrahydric, and higher polyhydric also- These compounds include among the polyfimctional acids and derivatives tricarballylic acid.

- citric acid, cyclic delta ketonic tetracarboxylic acids. such as are shown in United States Patent No, 2,329,432, issued September 14, 1943, benzene p'entacarboxylic acid, and mellitic acid, methyl, ethyl, or phenyl esters of such acids, trimethyl amine salts thereof, the simple amides, phosphite esters,-such as the aryl phosphites, alkyl phosphites, cycloalkyl phosphites, or aralkyl phosphites, examples of which are tricresyl phosphite, triphenyl phosphite, dibutylphenyl phosphite, phenyl ethyl phosphite, trimethyl phosphite, triethyl phosphite, trioctyl phosphite, diamyi phosphite, monoamyl phosphite, diphenoxyethyl phosphite, dicyclohexyl, and the corresponding thiophosphites, phosphate esters, examples of which are tricresyi phosphate, triethyl phosphate, triphenyl phosphate, triamyl phosphate, diphenyl ethyl phosphate, diphenyl phosphate, tri-p-butoxyethyl phosphate, and the like, triethyl borate, triamyi b'orate, tricapryl borate, arsenites, such as triethyl arsenite, triphenyl arsenite, etc. There may likewise be used phosphorus trichloride, phosphoric anhydride, phosphoric oxychloride,

v arsenic trioxide, etc.

ing agent used be an acid or derivative thereof.

At the same time, it should be pointed out that stabilizing action is not confined to the preferred conditions just recited. Thus. even with terminal ass-mac 6 linear polymers when a desired degree of condensation has been produced. There must be an opportunity for the added polyfunctional ester-forming material to react with terminal groups-of the already formed condensate. Of course, in causing reaction of the stabilizing agent with the condensate, some additional linear condensation will occur. This can be allowed for in the reaction schedule. When polymers of low or only moderate molecular weight are desired, the condensation before addition of stabilizing agent should be carried more nearly to the desired state than in the case of higher polymers. Specifically, in the case of phosphites as stabilizing agents and in the case of condensates having intrinsic viscositiesbelow about 0.7, the condensation may desirably be carried close to the desired state of polymerization before addition of stabilizing agent, as subsequent condensation takes place but slowly. Above 0.7, however, considerably more latitude .exists when phosphites are used as stabilizers and linear condensation may be safely carried onto the desired state at the same time that the stabilizing agent is being reacted. All in all, the exact time of addition of stabilizing agent is not critical. With due regard to the presence of catalysts, temperatures of reaction, and other conditions which bring about the formation of linear polyesters, it may be said that the addition of stabilizing agent may be made from about :oneand onehalf to three hours before completion of the condensation reaction and the reaction continued at a temperature sumcient to ensure reaction of reactive agents, such as pentaerythritol or trihydroxyl groups, there may be used polyhydric Y alcohols. By way of illustration, pentaerythrite has a definite stabilizing influence, although not as great, perhaps, as that obtained from triamyl phosphite or phosphorous acid.

The amount of ester-forming compound having I a functionality of at least three which isreacted with the linear condensate is small, 0.0015 to 0.075 gram mol of said ester-forming compound per kilogram of theoretical polymer being not only suflicient but also within such limits that excessive and undesirable changes in the nature'of the final polymer do not develop. It is'preferred that concentrations of 0.003 to 0.04 mol be used as in most cases with consideration of both reactants and particular stabilizer, an optimum stability an extent approaching that giving the properties desired for a given'appiicatiom Extremely early addition of stabilizing amounts of an ester-forming compound having a functionality of at least three is generally unfavorable to the continuation of linear'condensation. On the other hand, the-stabilizing compound cannot be merely mechanically fmixed with, but .not reacted with,.

phenyl phosphate,'temperatures of 180 to 300 C. are generally required.

Stabilization according to this invention becomes of increasing importance as the chain length of the polymer increases. As might be expected, lower polymers degrade to a smaller extent and usually less rapidly than the higher polymers. The stabilization of polymers having intrinsic viscosities above about 0.5 is of particular importance, for such polymershaveconsid-" erable tendency to degrade in air, light,- ormoisture, particularly when the polymers are acid catalyzed,

The stability of v according to this invention may be appraised by an accelerated test such as the following. -A sample of the polyrneris placed in a dishin an oven at C. for sixteen hours. Solutions arethen made of the heated sample and of the-original material. viscosities of each are determined.

From the change in viscosities of thesolutions .at the same concentration or from the change in the values of intrinsic viscosities, the degree of stabilization maybe evaluated. Comparison may be made with condensates ofabout the same original intrinsic'viscositybut which have not been reacted with a stabilizing amount of an ester-forming compound having a functionality above two.

The results of such an accelerated test have been compared with results obtained by natural polymeric products prepared.

viscosity was again determined and found to be in toughness and'flexibility was approximately proportional to the loss in intrinsic viscosity.

A similar sample of ethylene sebacate stabilized according to this invention had an initial intrinsic viscosity of 0.848. It was stored in the same cabinet for the same length of time as the unstabilized sample above. At the end of this time, the intrinsic viscosity was 0.809, representing a loss of only 0.039 unit.

A similar preparation stabilized according to this invention with 0.2% of tricapryl phosphite based on the weight of polymer had an initial intrinsic viscosity of 0.841. After being heated at 125 C. for fifteen hours, it had an intrinsic viscosity of 0.818, representing a loss of 0.023 unit, a value of the same order as that obtained above with natural aging for nineteen months.

Further details of this invention are presented in the following illustrative examples:

Example 1 A molecular proportion of sebacic acid was mixed with ethylene glycol in an amount greater than equivalent to the acid. The mixture was heated at 190-200 C. for approximately three and a half hours. During this time, glycol was refluxed from a condenser maintained at about 100 C. to facilitate the removal of water. The condenser was then removed, and the reaction mixture was heated under greatly reduced pressure with the temperature being gradually raised to about 265 C. The mixture was held at this temperature under 10 mm. mercury pressure until the desired degree of polymerization was reached (approximately twenty hours). The resulting polymer had an intrinsic viscosity of 0.9 as calculated by the formula:

viscosity ratio-1 Intrinsic viscosity o n c entrati on wherein the viscosity ratio is the viscosity of the solution of polymer divided by the viscosity of the solvent (both at 25 C.)

When this polymer was heated for sixteen hours at 125 0., it changed in intrinsic viscosity from 0.9 to 0.8.

The preparation of polymer was repeated under as nearly identical conditions as possible except that when the intrinsic viscosity approached a value of 0.8, 0.0015 mol of triphenyl phosphite per mol of sebacic acid was added thereto and the reaction continued until the intrinsic viscosity reached about 0.9.

A sample of this polymer was also heated for sixteen hours at 125 C. It changed in intrinsic viscosity only about 0.01 unit. Both the stabilizecl and unstabilized samples, before heating, were very tough and flexible, but these properties were retained only by the stabilized sample. The stabilized polymer was suitable for extrusion coating on wire.

Example 2 This is a useful and convenient formula, approximating in results the values obtained by the formula, intrinsic viscosity==log. ratio/concentration. Concentration is in grams per 100 cc. of solvent.

no longer freehr evolved. The reaction mixture was then heated under 10 to 20 mm. mercury pressure and the excess glycol distilled off. The condensate thus formed was heated under low pressure at 200-275 C. until an intrinsic viscosity of 0.940 was reached. A sample of this product heated in air at C. for sixteen hours changed in intrinsic viscosity to 0.736.

The above reaction was repeated, except that as the intrinsic viscosity rose above 0.7 there was added to the reaction mixture 0.0015 mol of triphenyl phosphite. The reaction was continued under reduced pressure until the intrinsic viscosity reached a value of 0.957. A sample of this polymer heated for sixteen hours at 125 C. dropped to 0.944.

Another preparation carried to an intrinsic viscosity of 0.764, after treatment with 0.0066 gram mol of triphenyl phosphite per kilogram of polymer, changed to 0.758 after being heated for sixteen hours at 125 C.

Example 3 The procedure of Example 2 was repeated except that tricapryi phosphite in an amount-of 0.27% (based 'on the resulting polyester), or 0.0015 mol, or 0.0066 gram mol per kilogram of polymer, was used in place of the triphenyl phosphite. The intrinsic viscosity was 0.841. After a sample was heated for sixteen hours at 125 C., the intrinsic viscosity thereof was 0.818.

Example 4 The procedure of the preceding examples was followedwith triphenylethyl phosphite at 0.25% (based on the polyester) or 0.0066 gram mol per kilogram of polymer as the stabilizing agent. The loss in intrinsic viscosity was 0.02 unit during the accelerated stability test.

Example 6 The procedure of the preceding examples was followed with tri-(diisobutylphenoxyethyl) phosphite as the stabilizing agent, 0.0015 mol being used. A change of intrinsic viscosity from 0.725 to t0.707 was found in the accelerated stability tes Example 7 Phosphorous acid in an amount of 0.05% (0.0015 mol) was used as a stabilizer. A polymer having an intrinsic viscosity of 0.634 dropped 0.016 unit, and one having an intrinsic viscosity of 0.809 dropped 0.027 unit when heated in the test for stability.

Example 8 Phosphorus trichloride was used as a stabilizer. Because of its volatility, 0.0033 mol was used per mol of sebacic acid. While considerable of this material was lost, the polymer obtained had excellent stability. The intrinsic viscosity fell from 0.797 to 0.744 during a standard stability test.

In all of the above examples, the polymers which had been treated with stabilizing agents retained their desirable properties when heated toughness.

inair andiin'llght. 'polymersre mained flexibleand tough, whereas samples which cam ehard and brittle. It'was iurther noted, that some stabilized samples retained their color much better than unstabllized polymers. R

It was noted that when an unstabilized polymer and a stabilized polymer gave. the same values Y "for intrinsic viscosity at 0.4. gram per 100 cc. of chloroform,- the viscosities of solutions in other hadinot been reacted with stabilizing asents bel sample "(0) A molecular proportion of succinic acid and an excess oi ethylene glycol over the theoretical requirement were mixed and heatedtogether. A trace of zinc chloride was added. Water was removed along with glycol. Finally, excess glycol was removed by heating under reduced pressure. The reaction temperature was carried up to about 225 C. while hydrogen was bubbled through the solvents might vary. Thus, at a. concentration of in ethylene dichloride, theviscositiesci the solutions of unstabilized polymers were generally greater than the viscosities of similar solutions or stabilized polymers having the same intrinsic'viscosities. The viscosities of melted stabilized polymers tended to-be but little more than for ten days at 60 C. Intrinsic viscosities were then determined. A'sebacic acid-glycol. polymer, catalyzed with zinc chloride, gave a value oi. 0.908

reaction mixture. The resulting polymer had an intrinsic viscosity of 0.522, which fell to 0.454

after the accelerated stability test in air.

' (b) The above preparation was repeated except that, at about an intrinsic viscosity of 0.5, there was introduced 0.0066 gram mol of trlphenyl phosphite per kilogram oi polymer and the heating v continued while hydrogen was bubbled through v veneers.

the reaction-mixture. A polymer of an intrinsic viscosity of 0.590 resulted, which fell to 0.574

after the accelerated stability test in air. This product was hard but tough and well suited ior sheets of material, such as wood laminating Erample 11 before'submersion and 0.702 aiter," and-hadlostits A o c a p opo ti n 01 azela c acid was A similar sample which had been stabilized with 0.003 gram mol of triphenyl phosphite per kilogram of polymerchanged from 0.842 to 0.785 without anyserious change in other 'properties. Another polyester stabilized with 0.2% of the same phosphitefchanged from 0.848 to 0.798 in intrinsic viscosity.

By procedures similar to those described above linear polymers were prepared in variet and stabilized with ester-forming compounds having a functionality or at least three. Definite stabiliza-' tion was evident when about 0.001'or more gram mols of such ester-forming compound was used per kilogram of polymer. With amounts of 0.0015 mol up to 0.075 mol, adequatev stabilization was obtained. Above the latter concentration, however, excessive gelation usually occurred, and the resulting polymers developed undesirablev properties, such as extremely high melt viscosities. In some cases at concentrations above 0.075 gram mol per kilogram oi theoretical polymer actual I impairment of stability". was, noted.

Example 9 (a) One molecularproportion of sebacic acid and an excess oipropylene'glycol were mixed and heated. Water was taken ofl and finally excess propylene glycol was removed under reduced pressure; About 0.1% of zinc chloride was added as a catalyst and the polymerization continued until an intrinsic viscosity of 0.777 was reached. The intrinsic viscosity fell to 0.631, when the polymer was heated for sixteen hours at 125 C. in air. (22). The preparation or polymeric propylene sebacate was repeated with the change that when the intrinsic viscosity reached about 0.7, 0.007

gram mol of tricresyl phosphite per kilogram of polymer was introduced and the reaction continued under an atmosphere of nitrogen until an intrinsic viscosity of 0.768 was reached. When a sample of this polymer was heated for sixteen hours at 125 0., the value for intrinsic viscosity I fell only 0.014 unit.

heated with a'large excess of dimethyl trimethylene glycol under reflux conditions. Zinc chloride was added in a catalytic amount, and the heating was continued under reduced pressure. The glycol was removed and the polymer heated until an intrinsic viscosity of about 0.7 wasreached. Tricresyl phosphate (0.075 gram mol per kilogram Example 12 The procedure of Example 2 was followed except that 0.0066 gram mol of triphenyl phosphate per kilogram of'polymer was used in place or the This product was compounded with butadiene- 'acrylonitrile synthetic rubber and found to impart remarkable flexibility atv low temperatures with no undesirable decrease in tensile strength or oil resistance.

phosphite. The intrinsic viscosity of the polymer was 0.795. After this polymer was heated at 125 C. for eighteen hours, the intrinsic viscosity was 0.773.

Example 18 The procedure of Examples 2 and 12 was followed except that o-phosphoric acid in an amount of 0.0075 mol per mol of acid was used as the stabilizing agent. The reaction was stopped when the intrinsic viscosity reached 0.798. A sample of. this polymeric material heated for sixteen hours at 125 C. in air gave an intrinsic viscosity of 0.668.

A preparation from the same materials was made parallel to the above stabilized preparation, but no stabilizing agent was added. This material showed an intrinsic viscosity of 0.811, which dropped to 0.582 after the stability test.

Example 14 One molecular proportion of sebacic acid and /100 molecular proportion of maleic anhydride were mixed with a 20% molecular excess of a mixture of parts ofethylene glycol and 20 parts of propylene glycol. The resulting mixture was heated under reflux conditions until water was no longer given oil. The reaction mixture was then heated under reduced pressure and the excess alcohols removed. There was then added triphenyl phosphite in an amount of 0.0015 mol. Heating under vacuum was continued at 220 C. until an intrinsic viscosity oi 1.10 was. reached.

11 After a sample of this polymeric material was heated in the "usual accelerated stability; test, it was: found to have an intrinsic viscosit ori-0.953. Aparallel preparation was--made, but without the useof astabilizer. The polymerization was carried on until an intrinsic viscosity of 1.10 was erties of long-chained linear polyesters and which is resistant to changes resulting from aging, air, moisture, or light. The new polymeric compositions possess a utility far beyond that of similar unstabilized polyesters and may be used in applications such as coating, laminating, extruding, and the like, for which comparable compositions known heretofore have been of less or even doubtful utility. They may also be used under conditions which preclude the use of previously known polyesters.

The hosphites have been found to possess a stabilizing action which is particularly valuable. At the same time, they have value as anti-oxidants. If desired, other anti-oxidants may be added to the polymeric compositions of this invention in addition to a polyfunctional stabilizing agent.

We claim:

1. In the stabilization against degradation in molecular weight of a polyester consisting of chains from a saturated dihydric alcohol with a carbon chain of two to twelve carbon atoms and alcoholic hydroxyl groups as the sole reactive functional groups thereof, chains from a saturated dicarboxylic acid with a chain of four to fourteen carbon atoms and with carboxyl groups as the sole reactive functional groups thereof, and chains from an oleflnically unsaturated aliphatic dicarboxylic acid with a chain of four to six carbon atoms and with carboxyl groups and an oleflnic linkage as the sole functional groups thereof, the number of chains from said unsaturated acid being less than the number of chains from said saturated acid, the steps which comprise reacting by condensing together under the influence of heat said alcohol and said acids with the saturated acid in molecular excess of the unsaturated acid until polyesterlflcation has taken place, then reacting under the influence of heat as the sole reactants the resulting polyester and from 0.0015 to 0.075 gram mole per kilogram of said polyester of a phosphorus compound from the group consisting of alkyl phosphite esters in which the alkyl group has one to eight carbon atoms and phenyl and alkylphenyl phosphite esters wherein the alkyl substituent is Joined to the phenyl group and contains one to eight carbon atoms.

2. In the stabilization against degradation in molecular weight of a polyester consisting of chains from a saturated dihydric alcohol with a carbon chain of two to twelve carbon atoms and alcoholic .hydroxyl groups as the sole reactive functional groups thereof, chains from a saturated dicarboxylic acid with a chain of four to fourteen carbon atoms and with carboxyl groups as their sole reactive functional groups thereof, and chains from an oleflnically unsaturated aliphatic dicarboxylic acid with a chain of four to six carbon atoms and with carboxyl groups and 12 an oleflnic linkage as the sole'functi onalgroup's thereof, the number ofchains from jsaidjunsat-T urated acid being less than the number of chains,

from said saturated acid, the steps whichcomprise reacting by condensing together Hnde'rth influence of heat said alcohol and said acids with the saturated acid in molecular excessof the unsaturated acid until polyesteriflcation has taken place, then reactingun'der the influence of heat as the sole reactants the resultingpolyester' and from 0.003 to 0.04 gram mole'per kilogram of said polyester of a phosphorus compound from the group consisting of alkyl phosphite esters in which the alkyl group has one to eight carbon atoms and phenyl and alkylphenyl phosphite esters wherein the alkyl substituent is joined to the phenyl group and contains one to eight carbon atoms.

3. In the stabilization against degradation in molecular weight of a polyester consisting of chains from a saturated dihydric alcohol with a carbon chain of two to twelve carbon atoms and alcoholic hydroxyl groups as the sole reactive functional groups thereof, chains from a saturated dicarboxylic acid with a chain or four to fourteen carbon atoms and with carboxyl groups as the sole reactive functional groups thereof, and chains from an oleflnically unsaturated aliphatic dicarboxylic acid with a chain of four to six carbon atoms and with carboxyl groups and an oleflnlc linkage as the sole functional groups thereof, the number of chains from said unsaturated acid being less than the number of chains from said saturated acid, the steps which comprise reacting by condensing together under the influence of heat said alcohol and said acids with the saturated acid in molecular excess of the unsaturated acid until polyesteriflcation has taken place, then reacting under the influence of heat as the sole reactants the resulting polyester and from 0.0015 to 0.075 gram mole per kilogram of said polyester of an alkylphenyl phosphite ester wherein the alkyl group is joined to the phenyl ring and contains one to eight carbon atoms.

4. In the stabilization against degradation in molecular weight of a polyester consisting of chains from a saturated dihydric alcohol with a carbon chain of two to twelve carbon atoms and alcoholic hydroxyl groups as the sole reactive functional groups thereof, chains from a saturated dicarboxylic acid with a chain of four to fourteen carbon atoms and with ca boxyl groups as the sole reactive functional groups thereof, and chains from an olefinically unsatu rated aliphatic dicarboxylic acid with a chain of four to six carbon atoms and with carboxyl groups and an oleflnic linkage as the sole functional groups thereof, the number of chains from said unsaturated acid being less than the number of chains from said saturated acid, the steps which comprise reacting by condensing together under the influence of heat said alcohol and said acids with the saturated acid in molecular excess of the unsaturated acid until polyesterification has taken place, then reacting under the influence of heat as the sole reactants the resulting polyester and from 0.0015 to 0.075 gram mole per kilogram of said polyester of an alkyl phosphite ester wherein the alkyl group contains one to eight carbon atoms.

5. In the stabilization against degradation in molecular weight of a polyester consisting of chainsfrom a saturated dihydric alcohol with a carbon chain of two to twelve carbon atoms and 13 alcoholic hydroxyl groups as the sole reactive functional groups thereof, chains from a saturated dicarboxylic acid with a chain of four to fourteen carbon atoms and with carboxyl groups as the sole reactive functional groups thereof, and chains from an olefinically unsaturated aliphatic dicarboxylic acid with a chain of four to six carbon atoms and with carboxyl groups and an olefinic linkage as the sole functional groups thereof, the number of chains from said unsaturated acid being less than the number of chains from said saturated acid, the steps which comprise reacting by condensing together under the influence of heat said alcohol and said acids with the saturated acid in molecular excess of the unsaturated acid until polyesterification has taken place, then reacting under the influence of heat as the sole reactants the resulting polyester and from 0.0015 to 0.075 gram mole per kilogram of said polyester of triphenyl phosphite.

6. In the stabilization against degradation in molecular weight of a polyester consisting of chains from a saturated dihydric alcohol with a carbon chain of two to twelve carbon atom and alcoholic hydroxyl groups as the sole reactive functional groups thereof, chains from a saturated dicarboxylic acid with a chain of four to fourteen carbon atoms and with carboxyl groups as the sole reactive functional groups thereof, and chains from an oleflnically unsaturated aliphatic dicarboxylic acid with a chain of four to six carbon atoms and with carboxyl groups and an olefinic linkage as the sole functional groups thereof, the number of chains from said unsaturated acid being less than the numberof chains from said saturated acid, the steps which comprise reacting by condensing together under the influence of heat said alcohol and said acids with the-saturated acid in molecular excess of the unsaturated acid until polyesterification has taken place, then reacting under the influence of heat as the sole reactants the resulting polyester and from 0.0015 to 0.075 gram mole per kilogram of said polyester of tricresyl phosphite.

7. In the stabilization against degradation in molecular weight of a polyester consisting of chains from a saturated dihydric alcohol having a chain of two to twelve carbon atoms and having alcoholic hydroxyl groups as the sole reactive functional groups and chains from sebacic acid and maleic acid, the number of chains from the sebacic acid being greater than the number of chains from the maleic acid, the steps which comprise reacting by condensing together under the influence of heat said alcohol and said acids with the saturated acid in molecular excess of the unsaturated acid until polyesteriflcation has taken place, then reacting under the influence of heat as the sole reactants the resulting polyester and from 0.0015 to 0.075 gram mole per kilogram of said polyester of a phosphorus compound from the group consisting of alkyl phosphite esters in which the alkyl group has one to eight carbon atoms and phenyl and alkylphenyl' phosphite esters wherein the alkyl substituent is joined to the phenyl group and contains one to eight carbon atoms.

8. The stabilized polyester resulting from the procedural steps of claim 7.

9. A process of stabilizing against. marked changes in molecular weight polyesters consisting of chains from a saturated dihydric alcohol with a. chain of two to twelve carbon atoms and alcoholic hydroxyl groups as the sole reactive functional group thereof, chains from a satuand chains from an oleflnically unsaturated ali- 14 rated dicarboxylic acid with a chain as the sole reactive functional groups thereof,

phatic dicarboxylic acid with a chain of four. to six carbon atoms and with carboxyl groups and an olefinic linkage as the sole functional groups thereof, the number of chains from said unsaturated acid being less than the number of chains from said saturated acid, which" comprises reacting by condensing under the influence of heat said acids with the saturated acid in molecular excess of the unsaturated acid and said alcohol in molecular excess-of the acids to form a polyester, continuing the condensation with removal of excess alcohol until a polyester of a molecular size from 3000 to 12,000 is obtained. adding to the polyester at a time one and a half to three hours before said molecular size is reached and reacting therewith 0.0015 to 0.075 gram mole per kilogram of the polyester of a phosphorus compound from the group consisting of alkyl phosphite esters in which the alkyl group has one to eight carbon atoms and phenyl and alkyl as the sole reactive functional groups thereof,

and chains from an oleflnically unsaturated aliphaticv dicarboxylic acid with a chain of fourto six carbon atoms and with carboxyl groups and an olefinic linkage as the sole functional grou s thereof, the number of chains from said unsaturated acid being less than the number of chains from said saturated acid, which comprises reacting by condensing under the influence of heat said acids with the saturated acid in molecular excess of the unsaturated acid and said alcohol in molecular excess of the acids to form a polyester, continuing the condensation with removal of excess alcohol until a polyester of a molecular size from 3000 to 12,000 is obtained, adding to the polyester at a time one and a half to three hours before said molecular size is reached and reacting therewith 0.0015 to 0.075 gram mole per kilogram of the polyester of an alykyl phosphite wherein the alkyl group contains one to eight carbon atoms. 7

11. A process of stabilizing against marked changes in molecular weight polyesters consisting of chains from a saturated dlhydric alcohol with a chain of two 'totwelve carbon atoms and alcoholic hydroxyl groups as the sole reactive functional groups thereof, chains-from a saturateddicarboxylic acid with a chain of four to fourteen carbon atoms and with carboxyl groups as the sole reactive functional groups thereof,

. phatic dicarboxylic acid with a chain of four to six carbon atoms and with carboxyl groups and an oleflnic linkage as the sole functional groups of four to fourteen carbon atoms and with carboxyl groups in molecular excess or the acids to form a polyester, continuing the condensation with removal of excess alcohol until a polyester 01 a molecular size from 3000 to 12,000 is obtained, adding to the polyester at a time one and a halt to three hours before said molecular size is reached and reacting therewith 0.0015 to 0.075 gram mole per kilogram of the polyester 01' triphenyl phosphite.

12. A process of stabilizing against marked changes in molecular weight polyesters consisting of chains from a saturated dihydric alcohol with a chain of two to twelve carbon atoms and alcoholic hydroxyl groups as the sole reactive functional groups thereof, chains from a saturated dicarboxylic acid with a chain of four to fourteen carbon atoms and with carboxyl groups as the sole reactive functional groups thereof, and chains from an olefinically unsaturated aliphatic dicarboxylic acid with a chain of four to six carbon atoms and with carboxyl groups and an oleflnic linkage as the sole functional groups thereof, the number of chains from said unsaturated acid being less than the number of chains from said saturated acid, which comprises reacting by condensing under the influence of heat said acids with the saturated acid in molecular excess of the unsaturated acid and said alcohol in molecular excess of the acids to form a polyester, continuing the condensation with removal or excess alcohol until a polyester 01' a molecular size from 3000 to 12,000 is obtained, adding to the polyester at a time one and a halt to three hours before said molecular size is reached and reacting therewith 0.0015 to 0.075 gram mole per kilogram of the polyester of tricresyl phosphite.

13. The stabilized polyester resulting from the procedural steps of claim 1. r

14. The stabilized polyester resulting from the process of claim 9.

DAVID A. ROTHROCK, JR. RICHARD F. CONYNE.

REFERENCES CITED The following references are of record in the file of this patent:

UNITED STATES PATENTS Number Name Date 1,970,510 Ellis Aug. 14, 1934 2,153,511 Cheetham et al Apr. 4, 1939 2,249,950 Fuller July 22, 1941 2,322,756 Wallder June 29, 1943 FOREIGN PATENTS Number Country Date 540,168 Great Britain Oct. 8, 1941 

